CN1104926C - Multifunctional enclosed continuous filter - Google Patents
Multifunctional enclosed continuous filter Download PDFInfo
- Publication number
- CN1104926C CN1104926C CN98120076A CN98120076A CN1104926C CN 1104926 C CN1104926 C CN 1104926C CN 98120076 A CN98120076 A CN 98120076A CN 98120076 A CN98120076 A CN 98120076A CN 1104926 C CN1104926 C CN 1104926C
- Authority
- CN
- China
- Prior art keywords
- filter
- casing
- scraper
- airtight continuous
- cloth
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The present invention relates to a filter which is used for solid and liquid separation, and has the advantages of high separation efficiency, continuous production and sealed operation, and simultaneously, is suitable for materials containing volatile flavour or (and) needing pressurizing and separating. The filter comprises a feed tube, a filter casing, a filter plate in different shapes and different operating modes, a motor, a drive device, a rectangular blade-shaped scraper, a liquid outlet tube, a rotating shaft, a solid discharge opening and a solid conveying device, wherein the filter casing is made of stainless steel or a carbon steel lining and is fixedly connected and sealed by a flange; the filter plate in different shapes and different operating modes is composed of three structures of a protective layer of a filter cloth, the filter cloth and a porous plate; the scraper is operated in different modes.
Description
The present invention relates to a kind of airtight continuous filter.More particularly, relate to that a kind of both to have had the unit volume filter area big, filter medium both sides pressure reduction is big, keep certain filter cake thickness, filtering rate is big, and the separative efficiency height again can serialization production, can also closed-loop operation be suitable for simultaneously containing selecting and send out the property smell, or/and need the filter of the material that pressurization separates.
As everyone knows, equipment for separating liquid from solid is an indispensable unit operating equipment in the industry such as chemical industry, metallurgy, coal, mine, medicine, weaving, papermaking, food, environmental protection.Up to now, existing separator is concluded and is mainly included the film separation and do not have membrane separation device, wherein have membrane separation device to be divided into: pressure filter, for example: sheet frame or box pressing filter, tubular type pressing filter, close press (claiming pressure leaf filter again), ultrafiltration membrance filter machine; Vacuum apparatus, for example: rotary drum filter, folder end filter, leaf-type filter, disc type (polydisc, single-deck) filter, bag type filtering machine, tubular filter; Filter centrifugal, for example: 3-foot (top discharge) filter, top suspension (bottom discharge) filter, 3-foot (scraper bottom discharge) filter, body formula (continous way) filter.
Above-mentioned various equipment for separating liquid from solid all has advantage and unsurmountable inherent shortcoming separately.For example, flame filter press is the widest a kind of filter of present purposes; Because of its unit volume filter area bigger, it imposes on the pressure differential of filter medium both sides can be greater than 760mmHg, this is just much bigger than the pressure differential of vacuum filter, and filter cake thickness is generally between 30mm～40mm, more stable, but its defective is that up to the present it can't filter in serialization, and every filter is once, take long to material loading, discharging, filter wash cloth, thus the volume that it is intrinsic advantage little, that separative efficiency is high has weakened; And its filter cake thickness is subjected to the restriction of filter frame thickness, is difficult to change, so its filtering rate is a process of successively decreasing, promptly speed is very fast at the beginning the time, but runs material easily, slows down along with the increase of filter cake thickness; The filter cake moisture content is also higher; Even blow also of no avail with compressed air.If with the filter cake attenuation, though can solve the problem that improves filtering rate, the time of loading and unloading is more frequent, and separative efficiency is poorer.In addition, this device is incomplete closed filter, and this certainly will cause and be difficult to be suitable for to contain volatile flavor, or/and need the separation of the material that pressurization separates, work situation is abominable, labour intensity strengthens thereby make.
The rotary drum vacuum filter of having many uses, though its energy continued operation, overcome the shortcoming that flame filter press can not continuous filtration, but its unit volume filter area is too little, the pressure reduction of filter medium both sides is also little, is far smaller than 760mmHg, and motive force is little, so filtering rate is little, separative efficiency also reduces; And this device is the filter of open type, does not fit into equally to contain volatile flavor, or/and need the separation of the material that pressurization separates, work situation is abominable, labour intensity strengthens thereby make.
Bag type filtering machine, it grows up on above-mentioned filter basis, and it can continuous filtration, vacuum and extruding can be combined again, has strengthened the pressure reduction of filter medium both sides, has increased filtering rate, and is more progressive to some extent than rotary drum filter.But its unit volume filter area little (similar defective being arranged) to rotary drum filter, obviously, it can not be compared with flame filter press; Moreover it is to the adaptability extreme difference of fine, and band decreases big; Be the filter of open type because of it, do not fit into equally and contain volatile flavor that or/and need the separation of the material that pressurization separates, work situation is abominable, labour intensity strengthens thereby make again.
Filter centrifugal has powerful centrifugal force, and intensity filter is improved greatly, but also continued operation, and but it is relatively poor to the adaptability of superfine material, particularly continuous centrifuge; Moreover the requirement of its process technology is high, the cost height, and maximization is had any problem; Be the filter of open type because of it, do not fit into equally and contain volatile flavor that or/and need the separation of the material that pressurization separates, work situation is abominable, labour intensity strengthens thereby make again.
The performance of the filter of other type is just poorer, has not enumerated one by one at this.So it is big to be badly in need of a kind of filter unit volume filter area that can keep of exploitation at present, filter medium both sides pressure reduction is big, filtering rate is big, the advantage that separative efficiency is high, and can overcome it again can not continued operation, can not make the filter cake attenuation, the novel filter of shortcoming that can not closed-loop operation.The present invention just is being based on that above-mentioned requirements arises at the historic moment.
The object of the present invention is to provide that a kind of both to have had the unit volume filter area big, filter medium both sides pressure reduction is big, keep certain filter cake thickness, filtering rate is big, the separative efficiency height, again can serialization production, can also the closed-loop operation simultaneous adaptation in the material that contains volatile flavor, or/and need the filter of the material that pressurization separates.
To achieve these goals, characteristics of the present invention provide the continuous filter of a kind of multifunctional airtight, and it comprises: feed pipe is used to make the material slurry to enter the pipeline of casing; Casing, the shell of filter; Filter is used for the filter medium of separation of material; Motor and transmission device are used for the power resources of filter; Scraper is used to scrape off the filter cake on the filter; Drain pipe, the filtrate that is used to pass filter is flowed out the outer pipeline of casing; Turning cylinder is used to make the axle of scraper rotation or the axle of filter rotation; The solid discharging opening, the outlet of the solid after being used to separate; Solids delivery device is used for the solid after separating is successively also released the outer spiral propeller of filter; It is characterized in that:
Described casing is by bearing-1～20Kg/cm
2That the stainless steel of pressure or carbon steel liner pressure-resistant material are made, the fixedly connected and airtight filter shell of usefulness ring flange;
Described filter, the difformity of forming by filter cloth protective layer, filter cloth and porous plate three-decker, the filter of different running method: wherein, described filter cloth protective layer is the ground floor of filter, and it can be selected from has cancellated stainless steel cloth, porous stainless steel sheet or nylon wire; Described filter cloth is the second layer of filter, and it can be selected from one deck cloth with permeability, uniform filter cotton and silk screen assembly or porous material plate; Described porous plate is the 3rd layer of filter, and it can be selected from porous metals, plastics or the ceramic material with rigid nature;
Described scraper is the cultrate scraper of rectangle, and it can turn round with the different modes of rotation, fixed or push-pull type: described scraper rotation is meant that scraper is fixed on the turning cylinder, and scraper rotates along with the rotation of turning cylinder; Described scraper fixed is meant that scraper is fixed on the casing, and the rotation along with filter scrapes filter cake; Described scraper push-pull type is meant that scraper is fixed on one and overlaps on the pull bar that can slide up and down, along with sliding up and down of pull bar scrapes filter cake;
Described scraper can make the filter cake thickness on the described filter remain in 0.1mm～10mm scope;
That described filter shape can be selected from is round, square, cartridge type, single face filter plate or two-sided filter plate;
The method of operation of described filter can be full immersion type, half immersion type and immersion type not: wherein said full immersion type is meant that each filter is parallel, vertically be arranged in the casing, and filter is fixed on the both sides of casing with a fixed bar, with screw filter is associated in drain pipe simultaneously, one of filter and scraper are fixed, another rotates, turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, pass from the filter center, whole filter is immersed in the slip, press vacuum plant to be positioned at the filter below as two edgings of described solids delivery device, link to each other with casing; During operation, scraper constantly scrapes the filter cake that produces on the filter, forms the below that deposit sinks to filter, falls into two edgings and presses on the vacuum plant, after this device is constantly extracted filter cake, outside the solid discharging opening is discharged casing;
Described half immersion type is meant that each filter is parallel, vertically is arranged in the casing, filter is connected on the turning cylinder, turning cylinder is fixed on the casing, turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, pass from the filter center, be connected with packing seal, end face seal sub-assembly with junction on every side at turning cylinder, scraper is fixed on the casing; During operation, half is immersed in filter in the slurries, under pressure promotes, solid-liquid is separated, solid forms filter cake and sticks on the filter, and along with the rotation of turning cylinder, air pressure makes filtrate pass filter cloth constantly outside drain pipe flows out casing, scraper constantly scrapes filter cake, and dried filter cake falls into spiral propeller and constantly is pushed out;
Described not immersion type is meant that each filter is parallel, transversely arranged in casing, form sandwich construction, connect with ring flange between every layer, filter is connected on the casing, with screw distributing device and scraper are connected on the turning cylinder, turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, passes from the filter center; During operation, slip flows into filter from distributing device, distributing device and scraper rotate along with the rotation of turning cylinder, under action of air pressure, filtrate is passed filter cloth and is flowed out outside the casing, the solid of staying filter forms filter cake, and scraper constantly scrapes filter cake, falls into spiral propeller and constantly is pushed out outside the casing;
The immersion type filter is provided with specially continuously extracts the solids delivery device of releasing outside the filter with the solid after separating, promptly two edgings are pressed vacuum plant, it comprises two screen pipes, and be connected on the casing with the packing seal sub-assembly, and motor and the transmission device outer with casing link to each other, under the drive of motor and transmission device, rotate simultaneously with counterclockwise and clockwise direction respectively, make material from the crack of described two screen pipes by being extruded, form big extruding force, filtrate enters in the described screen pipe and flows out by two surface filtration layer that roll, and after solid is extruded, along with the rotation of described screen pipe is got rid of filter cake outside the casing by the solid discharging opening;
Described screen pipe is made up of filter cloth protective layer, filter cloth and three layers of cylindrical configuration of antipriming pipe from outside to inside: wherein, described filter cloth protective layer is the ground floor of screen pipe, and it can be selected from has cancellated stainless steel cloth, porous stainless steel sheet or nylon wire; Described filter cloth is the second layer of screen pipe, and it can be selected from one deck cloth with permeability, uniform filter cotton and silk screen assembly or porous material plate; Described antipriming pipe is the 3rd layer of screen pipe, and it can be selected from porous metals, plastics or the ceramic material with rigid nature;
The immersion type filter is not provided with the feeding device of distributing device specially, it is the pipe of a bottom opening, slurry by described Pipe Flow to filter, described pipe is fixed on the turning cylinder and with scraper, rotate along with the turning cylinder rotation, simultaneously slip is evenly distributed on the filter,, and guarantees filtering rate with the thickness of control filter cake.
The present invention compares the useful effect that is had with background technology as follows:
According to the present invention, because casing is by bearing-1～20Kg/cm
2That the stainless steel of pressure or carbon steel liner pressure-resistant material are made, as to use the fixedly connected and airtight filter of ring flange shell, therefore, when filtration contain various peculiar smell, poisonous, volatile material arranged, or/and when needing material that pressurization separates, certainly will improve work situation, reduce labour intensity.
As everyone knows, the superiority key of the performance of evaluation filter is exactly to see its filtering rate.Filtering rate depends primarily on material performance, and when material performance one timing, filtering rate depends on the pressure differential of filter medium both sides and the thickness of filter cake, and promptly filtering rate is directly proportional with magnitude of pressure differential, is inversely proportional to filter cake thickness.Therefore strengthen pressure reduction and reduce the two big key elements that filter cake thickness just becomes improved filter performance.
The present invention has the filter of three-decker just by employing, because the filter cloth protective layer can protect filter cloth not scratched by scraper, make filter cloth that long benefiting from the life-span be arranged, and make it guarantee certain thickness filter cake on the one hand, have certain effect to preventing to wear to filter, and can long-time continuous filter; Porous plate is supporting filter cloth and can bear pressure on the other hand, when scraper scrapes off filter cake continuously, the filter cake thickness on the filter is remained in 0.1mm～10mm scope, keep filtering fast thereby significantly reduce resistance, the steady running time is long more, thereby the performance of serialization advantage is abundant more; And, make filter cake keep the state of relative thin, can guarantee that filter can not occur in running continuously that filter cake thickens and situation that filtering rate slows down.
And, slush pump of the present invention and/or air compressor machine, vacuum power, flocculant settling capacity and/or two edging are pressed vacuum plant and/or spiral propeller, act synergistically on the filter medium both sides, filter medium both sides pressure reduction is increased, guaranteed that filter has higher filtering rate, thereby kept the filter continuous operation.
Distributing device rotates along with the turning cylinder rotation with scraper, simultaneously slip is evenly distributed on the filter plate, with the thickness of control filter cake, and guarantees filtering rate; Press vacuum plants or spiral propeller continuously to release outside the filter as the two edgings of solids delivery device, to keep the filter continuous operation falling into the filter cake that solid connects material on the wall.
The vertical or horizontal sandwich construction of filter improves the filter area of filter unit volume greatly.
Therefore, because unit volume filter area of the present invention is big, the pressure reduction of filter medium both sides is big, and filter cake is thin, so the separative efficiency of filter is improved greatly.And this closed continuous operation has been simplified operation sequence greatly, and manual labor reduces, even the material of high-temperature operation, effumability, the operation of the material that need pressurize are also adapted to, and working environment is greatly improved, and welcome by operating personnel.
Specifically describe embodiments of the invention below in conjunction with accompanying drawing.
The structural representation of the filter of the full immersion type filter of Fig. 1;
The structural representation of the filter of Fig. 2 half immersion type filter;
The right side schematic diagram of the filter of Fig. 3 half immersion type filter;
Fig. 4 is the structural representation of the filter of immersion type filter not.
As shown in Figure 1, when the method for operation of filter is full immersion type: open electronic and transmission device 4, slurries are squeezed into feed pipe 1 by slush pump and are entered in the casing 2, increase along with slip, pressure in the casing also increases thereupon, the interior outside at filter 3 produces pressure reduction, liquid in the slurries will pass the filter medium on the filter plate at this moment, enter drain pipe 9 and flow out casings, and solid be filtered the plate resistance retaining, form filter cake on the filter surface, when filter cake increases to certain thickness,, make filter cake keep certain thickness (0.5～5mm) along with the scraper 5 of turning cylinder 7 rotations scrapes the filter cake thick-layer, it is very little that thereby the filtration resistance that makes filtering layer becomes, and kept high filtering rate.The filter cake that scrapes off falls into two edgings of casing 8 supports and presses on the vacuum plants 6, press vacuum plant further to extract through two edgings, the filter cake of being extracted is pressed the rotation of vacuum plant along with two edgings and is discharged outside the casing, scrape through scraper 10, discharge outside the casing from solid discharging opening 11, so far, the slurries that enter filter just are split up into filtrate and filter cake, finished the separation process of the solid and the liquid of slurries, so constantly enter slurries, constantly separating filtrate and filter cake again, thus realized the purpose of airtight continuous filtration.
The performance parameter of the full immersion type filter that now will be as shown in Figure 1 and the flame filter press of prior art is listed table 1 in.
Table 1
As shown in Figures 2 and 3, when the method for operation of filter is half immersion type: open motor and transmission device 8, enter in the casing 1 after with slush pump slip being squeezed into feed pipe 6, open air compressor machine simultaneously, also enter in casing through compressed air inlet 7 air, continuous increase along with slurries, filter 2 Lower Halves are soaked, under the effect of slush pump and air compressor machine, liquid in the slurries passes the filter medium on the filter plate, enter center rotating shaft 3 and outside liquid outlet 9 flows out casings, filter cake thickens on filter plate gradually, rotation along with turning cylinder, under the air pressure effect, liquid continues across the filter medium on the filter plate, enter center rotating shaft, and together outside liquid outlet flows out casing, the liquid in the filter cake further reduces, when moisture content reaches requirement, scraped by scraper 4, and make filter cake keep certain thickness (0.1～10mm), enter in the spiral propeller 5, discharge outside the casings from solid discharging opening 10, thereby finished the separation process of liquid and solid in the slurries, filter constantly rotates, and liquid and solid are just constantly separated, thereby reaches the purpose of liquid-solid separation.
Now the performance parameter of the vacuum-type drum filter of half immersion type filter shown in Fig. 2 and 3 and prior art is listed table 2 in.
Table 2
As shown in Figure 4, when the method for operation of filter is not during immersion type: at first open air compressor machine, make the compressed air intlet 1 of compressed air enter casing 2, make that pressure reaches required filter pressure (0.2～5Kg/cm in the filtration
2), open motor and transmission device 11 then, turning cylinder 6 is rotated, start slush pump this moment, the slip that needs filter is squeezed into feed pipe 9, enter the turning cylinder that links to each other with feed pipe with ring flange 10 again, enter distributing device 5 then, slurries are distributed on the filter 4 equably, slurries are subjected to the pressure effect of air compressor machine, then filtrate is passed the filter medium on the filter plate, enter liquid valve (pipe) 12 and flow out casing, and solids forms filter cake on filter, this filter cake is scraped by the scraper 3 along with the turning cylinder rotation, and make filter cake keep certain thickness (0.1～10mm), fall into spiral propeller 7, and be pushed out outside the casing from solid discharging opening 8, slip constantly enters, filtrate is constantly discharged with filter cake and is separated, thereby forms an airtight continuous filtration process.
The performance parameter of the not immersion type filter that now will be as shown in Figure 4 and the disk filter of prior art is listed table 3 in.
Table 3
The data of summary table 1, table 2 and table 3 can further draw the result as following table 4:
Table 4
Can find out obviously that from above-mentioned respectively the group the data unit volume filter area of I type machine is than the big 0.4m of flame filter press
2/ m
3, than the big 6.48m of rotary drum filter
2/ m
3, than the big 6.37m of disk filter
2/ m
3The unit volume filter area of II type machine is than the little 0.5m of flame filter press
2/ m
3, than the big 5.58m of rotary drum filter
2/ m
3, than the big 5.47m of disk filter
2/ m
3The unit volume filter area of III type machine is than the little 1.17m of flame filter press
2/ m
3, than the big 4.91m of rotary drum filter
2/ m
3, than the big 4.8m of disk filter
2/ m
3
This shows that the unit volume filter area of the flame filter press of maximum unit volume filter area is close in unit volume filter area of the present invention and the existing filter, bigger 10～16 times than other existing filter; Filter cake thickness of the present invention is littler 6～8 times than existing filter cake thickness; The pressure differential of filter medium of the present invention both sides is 2～17 times of pressure differential of existing filter filter medium both sides.
Therefore, because unit volume filter area of the present invention is big, the pressure reduction of filter medium both sides is big, and filter cake is thin, so the separative efficiency of filter is good.Just can learn from table 4: the separative efficiency of I type machine is 6.9 times of flame filter press, is 16 times of rotary drum filter, is 13.8 times of disk filter; The separative efficiency of II type machine is 10 times of flame filter press, is 23.8 times of rotary drum filter, is 20 times of disk filter; The separative efficiency of III type machine is 2.1 times of flame filter press, is 5 times of rotary drum filter, is 4.2 times of disk filter.
This shows that the separative efficiency of filter of the present invention is better than existing various filter greatly.
And, because casing is by bearing-1～20Kg/cm
2That the stainless steel of pressure or carbon steel liner pressure-resistant material are made, as to use the fixedly connected and airtight filter of ring flange shell, therefore, when filtration contain various peculiar smell, poisonous, volatile material arranged, or/and when needing material that pressurization separates, certainly will improve work situation, reduce labour intensity.
Simultaneously, by adopting filter of the present invention, on the one hand because the filter cloth protective layer can protect filter cloth not scratched by scraper, make filter cloth that long benefiting from the life-span be arranged, and make it guarantee certain thickness filter cake, have certain effect to preventing to wear to filter, and can long-time continuous filter; Porous plate is supporting filter cloth and can bear pressure on the other hand, when scraper scrapes off filter cake continuously, the filter cake thickness on the filter is remained in 0.1mm～10mm scope, keep filtering fast thereby significantly reduce resistance, the steady running time is long more, thereby the performance of serialization advantage is abundant more; And, make filter cake keep the state of relative thin, can guarantee that filter can not occur in running continuously that filter cake thickens and situation that filtering rate slows down.
Slush pump of the present invention and/or air compressor machine, vacuum power, flocculant settling capacity and/or two edging are pressed vacuum plant and/or spiral propeller, act synergistically on the filter medium both sides, filter medium both sides pressure reduction is increased, guaranteed that filter has higher filtering rate, thereby kept the filter continuous operation.
Distributing device rotates along with the turning cylinder rotation with scraper, simultaneously slip is evenly distributed on the filter plate, with the thickness of control filter cake, and guarantees filtering rate; Press vacuum plants or spiral propeller continuously to release outside the filter as the two edgings of solids delivery device, to keep the filter continuous operation falling into the filter cake that solid connects material on the wall.
The vertical or horizontal sandwich construction of filter improves the filter area of filter unit volume greatly.
Therefore, because unit volume filter area of the present invention is big, the pressure reduction of filter medium both sides is big, and filter cake is thin, so the separative efficiency of filter is improved greatly.And this closed continuous operation has been simplified operation sequence greatly, and manual labor reduces, even the material of high-temperature operation, effumability, the operation of the material that need pressurize are also adapted to, and working environment is greatly improved, and welcome by operating personnel.
Obviously, the present invention has realized aforesaid goal of the invention, provide promptly that a kind of both to have had the unit space filter area big, filter medium both sides pressure reduction is big, keeps certain filter cake thickness, and filtering rate is big, the separative efficiency height, again can serialization production, can also the closed-loop operation simultaneous adaptation in the material that contains volatile flavor, or/and need the filter of the material that pressurization separates.
Claims (36)
1. airtight continuous filter comprises: feed pipe; Casing; Filter; Motor and transmission device; Scraper; Drain pipe; Turning cylinder; The solid discharging opening; Solids delivery device; It is characterized in that:
Described casing is by bearing-1～20Kg/cm
2That the pressure-resistant material of pressure is made, the fixedly connected and airtight filter shell of usefulness ring flange;
Described filter, the difformity of forming by filter cloth protective layer, filter cloth and porous plate three-decker, the filter of different running method; Wherein said filter cloth protective layer is the ground floor of filter, and it can be selected from has cancellated material; Described filter cloth is the second layer of filter, and it can be selected from the material with permeability; Described porous plate is the 3rd layer of filter, and it can be selected from the material with rigid nature;
Described scraper is the cultrate scraper of rectangle, and it can turn round with different modes.
2. airtight continuous filter as claimed in claim 1, wherein said casing is to be made by stainless steel material.
3. airtight continuous filter as claimed in claim 1, wherein said casing is to be made by the carbon steel liner material.
4. airtight continuous filter as claimed in claim 1, wherein said filter shape can be selected from round.
5. airtight continuous filter as claimed in claim 1, wherein said filter shape can be selected from square.
6. airtight continuous filter as claimed in claim 1, wherein said filter shape can be selected from cartridge type.
7. airtight continuous filter as claimed in claim 1, wherein said filter shape can be selected from the single face filter plate.
8. airtight continuous filter as claimed in claim 1, wherein said filter shape can be selected from two-sided filter plate.
9. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth protective layer can be selected from has cancellated stainless steel cloth.
10. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth protective layer can be selected from has cancellated porous stainless steel sheet.
11. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth protective layer can be selected from has cancellated nylon wire.
12. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth can be selected from one deck cloth with permeability.
13. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth can be selected from the uniform filter cotton with permeability and the assembly of silk screen.
14. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said filter cloth can be selected from the porous material plate with permeability.
15. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said porous plate can be selected from the porous metals with rigid nature.
16. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said porous plate can be selected from the plastics with rigid nature.
17. as claim 1, one of 4,5,6,7,8 described airtight continuous filters, wherein said porous plate can be selected from the ceramic material with rigid nature.
18. airtight continuous filter as claimed in claim 1, the method of operation of wherein said filter can be full immersion type, wherein said full immersion type is meant that each filter is parallel, vertically be arranged in the casing, and filter is fixed on the both sides of casing with a fixed bar, with screw filter is associated in drain pipe simultaneously, one of filter and scraper are fixed, another rotates, turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, pass from the filter center, whole filter is immersed in the slip, presses vacuum plant to be positioned at the filter below as two edgings of described solids delivery device, links to each other with casing; During operation, scraper constantly scrapes the filter cake that produces on the filter, forms the below that deposit sinks to filter, falls into two edgings and presses on the vacuum plant, after this device is constantly extracted filter cake, outside the solid discharging opening is discharged casing.
19. airtight continuous filter as claimed in claim 1, the method of operation of wherein said filter can be half immersion type, described half immersion type is meant that each filter is parallel, vertically is arranged in the casing, filter is connected on the turning cylinder, and turning cylinder is fixed on the casing, and turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, pass from the filter center, in turning cylinder and junction packing seal on every side, the end face seal sub-assembly is connected, and scraper is fixed on the casing; During operation, half is immersed in filter in the slurries, under pressure promotes, solid-liquid is separated, solid forms filter cake and sticks on the filter, and along with the rotation of turning cylinder, air pressure makes filtrate pass filter cloth constantly outside drain pipe flows out casing, scraper constantly scrapes filter cake, and dried filter cake falls into spiral propeller and constantly is pushed out outside the casing.
20. airtight continuous filter as claimed in claim 1, the method of operation of wherein said filter can be an immersion type not, described not immersion type is meant that each filter is parallel, transversely arranged in casing, form sandwich construction, connect with ring flange between every layer, filter is connected on the casing, with screw distributing device and scraper is connected on the turning cylinder, turning cylinder is positioned at filter central authorities and perpendicular to the filter plane, passes from the filter center; During operation, slip flows into filter from distributing device, distributing device and scraper rotate along with the rotation of turning cylinder, under action of air pressure, filtrate is passed filter cloth and is flowed out outside the casing, the solid of staying filter forms filter cake, and scraper constantly scrapes filter cake, falls into spiral propeller and constantly is pushed out outside the casing.
21. airtight continuous filter as claimed in claim 1, the drive manner of wherein said scraper can be a rotation, and described scraper rotation is meant that scraper is fixed on the turning cylinder, and scraper rotates along with the rotation of turning cylinder.
22. airtight continuous filter as claimed in claim 1, the drive manner of wherein said scraper can be a fixed, and described fixed is meant that scraper is fixed on the casing, and the rotation along with filter scrapes filter cake.
23. airtight continuous filter as claimed in claim 1, the drive manner of wherein said scraper can be a repulsive-type maglev, and described repulsive-type maglev is meant that scraper is fixed on one and overlaps on the pull bar that can slide up and down, along with sliding up and down of pull bar scrapes filter cake.
24. as claim 1, one of 18,19,20 described airtight continuous filters, wherein said scraper can make the filter cake thickness of described filter remain in 0.1mm～10mm scope.
25. airtight continuous filter as claimed in claim 18, wherein said pair of edging presses vacuum plant to comprise two screen pipes, and be connected on the casing with the packing seal sub-assembly, and motor and the transmission device outer with casing link to each other, under the drive of motor and transmission device, rotate simultaneously with counterclockwise and clockwise direction respectively, make material from the crack of described two screen pipes by being extruded, form big extruding force, filtrate enters in the described screen pipe and flows out by two surface filtration layer that roll, and after solid is extruded, along with the rotation of described screen pipe is got rid of filter cake outside the casing by the solid discharging opening.
26. airtight continuous filter as claimed in claim 25, wherein said screen pipe are made up of filter cloth protective layer, filter cloth and three layers of cylindrical configuration of antipriming pipe from outside to inside; Described filter cloth protective layer is the ground floor of screen pipe, and it can be selected from has cancellated material; Described filter cloth is the second layer of screen pipe, and it can be selected from the material with permeability; Described antipriming pipe is the 3rd layer of screen pipe, and it can be selected from the material with rigid nature.
27. can being selected from, airtight continuous filter as claimed in claim 26, wherein said filter cloth protective layer have cancellated stainless steel cloth.
28. can being selected from, airtight continuous filter as claimed in claim 26, wherein said filter cloth protective layer have cancellated porous stainless steel sheet.
29. can being selected from, airtight continuous filter as claimed in claim 26, wherein said filter cloth protective layer have cancellated nylon wire.
30. airtight continuous filter as claimed in claim 26, wherein said filter cloth can be selected from one deck cloth with permeability.
31. airtight continuous filter as claimed in claim 26, wherein said filter cloth can be selected from uniform filter cotton and the silk screen assembly with permeability.
32. airtight continuous filter as claimed in claim 26, wherein said filter cloth can be selected from the porous material plate with permeability.
33. airtight continuous filter as claimed in claim 26, wherein said antipriming pipe can be selected from the porous metals with rigid nature.
34. airtight continuous filter as claimed in claim 26, wherein said antipriming pipe can be selected from the plastics with rigid nature.
35. airtight continuous filter as claimed in claim 26, wherein said antipriming pipe can be selected from the ceramic material with rigid nature.
36. airtight continuous filter as claimed in claim 20, wherein said distributing device is the pipe of a bottom opening, slurry by described Pipe Flow to filter, described pipe is fixed on the turning cylinder and with scraper, rotate along with the turning cylinder rotation, simultaneously slip is evenly distributed on the filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98120076A CN1104926C (en) | 1998-10-06 | 1998-10-06 | Multifunctional enclosed continuous filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98120076A CN1104926C (en) | 1998-10-06 | 1998-10-06 | Multifunctional enclosed continuous filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1249957A CN1249957A (en) | 2000-04-12 |
| CN1104926C true CN1104926C (en) | 2003-04-09 |
Family
ID=5226587
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98120076A Expired - Fee Related CN1104926C (en) | 1998-10-06 | 1998-10-06 | Multifunctional enclosed continuous filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1104926C (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6790653B2 (en) * | 2001-08-23 | 2004-09-14 | Bio-Reaction Industries, Llc | Biological filter apparatus with multiple filter units |
| CN103349857A (en) * | 2013-07-18 | 2013-10-16 | 安庆市虹泰新材料有限责任公司 | Plate frame type pressure filter for pressure filtering of dimer acid |
| CN113644868A (en) * | 2020-07-22 | 2021-11-12 | 郭萌萌 | Device for adjusting angle of solar power generation panel and using method |
| CN112795207A (en) * | 2020-12-19 | 2021-05-14 | 浙江恩盛染料化工有限公司 | Post-treatment method of disperse blue 60 |
| CN113694608B (en) * | 2021-08-18 | 2022-12-13 | 盛丽琼 | Water pollution treatment device convenient for quick connection of pipelines |
| CN116272089B (en) * | 2023-05-17 | 2023-08-18 | 新乡市中汇过滤技术有限公司 | Automatic slag discharging filter |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0224000A1 (en) * | 1985-10-22 | 1987-06-03 | Zwag AG | Filtration device, in particular of the Nutsche type |
| CN1084425A (en) * | 1992-09-24 | 1994-03-30 | 成都科技大学 | Continuous pressing filter |
| EP0655268A2 (en) * | 1993-11-30 | 1995-05-31 | Joachim Dipl.-Ing. Geldmacher | Filter for continuous filtering liquids which contain solids in a closed cylindrical container |
-
1998
- 1998-10-06 CN CN98120076A patent/CN1104926C/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0224000A1 (en) * | 1985-10-22 | 1987-06-03 | Zwag AG | Filtration device, in particular of the Nutsche type |
| CN1084425A (en) * | 1992-09-24 | 1994-03-30 | 成都科技大学 | Continuous pressing filter |
| EP0655268A2 (en) * | 1993-11-30 | 1995-05-31 | Joachim Dipl.-Ing. Geldmacher | Filter for continuous filtering liquids which contain solids in a closed cylindrical container |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1249957A (en) | 2000-04-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106396331B (en) | A kind of sludge concentration and dewatering desiccation integral processing unit and its processing method | |
| WO1998025684A1 (en) | Apparatus for continuous purification of liquids, dewatering and drying of the separated solids | |
| CN103697679A (en) | Solid and liquid separating, dehydrating and drying integrating machine | |
| CN1104926C (en) | Multifunctional enclosed continuous filter | |
| US4208188A (en) | Consolidation of coal slurry | |
| CN105923978B (en) | A kind of deeply dehydrating sludge processing unit and its processing method | |
| CN100420504C (en) | Belt type pressure filter | |
| WO1987004114A1 (en) | Dehydratation method and apparatus | |
| CN111420437B (en) | Vacuum filter | |
| CN107670966B (en) | Rotary powder screening machine | |
| CN1030434C (en) | Mechanical extruding type continuous filter press | |
| CN209348227U (en) | Belt, which is pressurizeed, air-dries filter | |
| CN200957323Y (en) | Belt pressurized filter | |
| CN213652240U (en) | Rotary extrusion type sludge treatment equipment | |
| CN107540190A (en) | A kind of drum-type dewaterer | |
| CN201091810Y (en) | Auger convey discharge forcing ceramic filter | |
| CN221358853U (en) | Device for continuously pressurizing and hermetically filtering catalyst slurry | |
| CN108751591A (en) | A kind for the treatment of method of printing and dying wastewater and system | |
| CN216571900U (en) | Efficient pressurization vacuum dehydration equipment | |
| CN101352626B (en) | Special type separation filter | |
| CN102989233A (en) | Continuous filtration method for polyacrylonitrile pulp | |
| CN1220908A (en) | Dewatering method-ultrafiltration dewatering | |
| KR102461500B1 (en) | Compressive Typed Dehydrating Machine Using Hiper Pressure | |
| CN209317172U (en) | A kind of continous way separating dry space from moist space device | |
| CN218951218U (en) | Negative pressure sludge treatment machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |